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Artykuły w czasopismach na temat "Fluidized-bed combustion Mathematical models"
Saxena, S. "Mathematical models for fluidized-bed coal combustion and sulfur retention". Energy 13, nr 7 (lipiec 1988): 557–607. http://dx.doi.org/10.1016/0360-5442(88)90011-4.
Pełny tekst źródłaWang, Zhong Jie, Ning Han i Jia Wang. "The Study on the Fuzzy Control Algorithm for Main Steam Pressure Control of Circulated Fluidized Bed Boiler". Advanced Materials Research 383-390 (listopad 2011): 2092–96. http://dx.doi.org/10.4028/www.scientific.net/amr.383-390.2092.
Pełny tekst źródłaMa, Yunpeng, Chenheng Xu, Hua Wang, Ran Wang, Shilin Liu i Xiaoying Gu. "Model NOx, SO2 Emissions Concentration and Thermal Efficiency of CFBB Based on a Hyper-Parameter Self-Optimized Broad Learning System". Energies 15, nr 20 (18.10.2022): 7700. http://dx.doi.org/10.3390/en15207700.
Pełny tekst źródłaMladenovic, Milica, Stevan Nemoda, Mirko Komatina i Dragoljub Dakic. "Numerical simulation of non-conventional liquid fuels feeding in a bubbling fluidized bed combustor". Thermal Science 17, nr 4 (2013): 1163–79. http://dx.doi.org/10.2298/tsci121116007m.
Pełny tekst źródłaWang, Liu, Zhang, Zhang i Jin. "Numerical Investigation of Solid-Fueled Chemical Looping Combustion Process Utilizing Char for Carbon Capture". Processes 7, nr 9 (6.09.2019): 603. http://dx.doi.org/10.3390/pr7090603.
Pełny tekst źródłaMei, Joseph S., Esmail R. Monazam i Lawrence J. Shadle. "Flow Regime Study of a Light Material in an Industrial Scale Cold Flow Circulating Fluidized Bed". Journal of Energy Resources Technology 128, nr 2 (22.03.2006): 129–34. http://dx.doi.org/10.1115/1.2199566.
Pełny tekst źródłaShimizu, Tadaaki, Mirko Peglow, Kazuaki Yamagiwa i Masato Tanaka. "Comparison among attrition-reaction models of SO2 capture by uncalcined limestone under pressurized fluidized bed combustion conditions". Chemical Engineering Science 58, nr 13 (lipiec 2003): 3053–57. http://dx.doi.org/10.1016/s0009-2509(03)00157-x.
Pełny tekst źródłade Lasa, Hugo. "The CREC Fluidized Riser Simulator a Unique Tool for Catalytic Process Development". Catalysts 12, nr 8 (12.08.2022): 888. http://dx.doi.org/10.3390/catal12080888.
Pełny tekst źródłaHajra, Sugato, i Abhishek Aditya Patra. "STUDY OF CIRCULATING COAL FLUIDIZED BOILERS". International Journal of Students' Research in Technology & Management 3, nr 6 (30.09.2015): 396. http://dx.doi.org/10.18510/ijsrtm.2015.363.
Pełny tekst źródłaKhasanov, I. R., A. V. Karpov, S. F. Lobova i N. V. Petrova. "Field modeling of the fire dynamics as an answer to the question about the fire alarm performance". Pozharovzryvobezopasnost/Fire and Explosion Safety 29, nr 5 (2.12.2020): 40–50. http://dx.doi.org/10.22227/pvb.2020.29.05.40-50.
Pełny tekst źródłaRozprawy doktorskie na temat "Fluidized-bed combustion Mathematical models"
Wildegger-Gaissmaier, Anna Elisabeth. "Fluidized bed utilization of South Australian coals". Title page, contents and abstract only, 1988. http://web4.library.adelaide.edu.au/theses/09PH/09phw672.pdf.
Pełny tekst źródłaAlagoz, Duriye Ece. "Mathematical Modeling Of Fluidized Bed Combustors With Radiation Model". Master's thesis, METU, 2006. http://etd.lib.metu.edu.tr/upload/12607489/index.pdf.
Pełny tekst źródłaBell, Robyn Anne, i Robyn Bell@csiro au. "Numerical modelling of multi-particle flows in bubbling gas-solid fluidised beds". Swinburne University of Technology, 2000. http://adt.lib.swin.edu.au./public/adt-VSWT20050902.132803.
Pełny tekst źródłaGogolek, Peter Edmund Gordon. "Mathematical modelling of fluctuations in fluidized bed combustion". Thesis, National Library of Canada = Bibliothèque nationale du Canada, 1998. http://www.collectionscanada.ca/obj/s4/f2/dsk2/tape17/PQDD_0006/NQ31928.pdf.
Pełny tekst źródłaAltindag, Hakan. "Mathematical Modeling Of Sulfur Retention In Fluidized Bed Combustors". Master's thesis, METU, 2003. http://etd.lib.metu.edu.tr/upload/1085661/index.pdf.
Pełny tekst źródłaAfacan, Onur M. "Mathematical Modeling Of Nox Emissions In Bubbling Fluidized Bed Combustors". Master's thesis, METU, 2005. http://etd.lib.metu.edu.tr/upload/12606463/index.pdf.
Pełny tekst źródłaChevrier, Solène. "Development of subgrid models for a periodic circulating fluidized bed of binary mixture of particles". Phd thesis, Toulouse, INPT, 2017. http://oatao.univ-toulouse.fr/19905/1/CHEVRIER_Solene.pdf.
Pełny tekst źródłaAsthana, Abhishek. "Modélisation mathématique de la formation des NOx et de la volatilisation des métaux lourds lors de l'incinération sur grille d'ordures ménagères". Thesis, Vandoeuvre-les-Nancy, INPL, 2008. http://www.theses.fr/2008INPL018N/document.
Pełny tekst źródłaAs a tool for controlling the Municipal Solid Waste (MSW) incineration process and its possible pollutant emissions, a mathematical model of the MSW bed burning on travelling grate of an incinerator was developed. The model describes most of the physico-chemical and thermal phenomena taking place in incineration like the drying and pyrolysis of the feed, combustion and gasification of char, oxidation of pyrolysis gases, heat transfer, bed shrinking, feed stirring, etc. Also described in the model are the mechanisms of Heavy Metals (HM) volatilization and NOx formation. Kinetics of HM release was modelled using the approach of additive reaction times accounting for the various transport mechanisms involved: external transfer, intra-particle diffusion and actual volatilization. In the case simulated, i.e. of Cd, almost total volatilization is predicted, which is confirmed by literature findings. The NOx sub-model takes into account most of the common mechanisms of formation like thermal, prompt, fuel, N2O intermediate and also NOx reduction by homogeneous reburning and heterogeneous reduction by char. Calculations show that NOx formation is predominated by the fuel mechanism and destruction by the heterogeneous reduction. Finally, the bed model was applied to study the influence of various operating parameters like flow rate, temperature and distribution of air under grates, waste particle size, feed stirring and the stirring scheme. The results are presented and discussed in detail and the influence of operating conditions on process efficiency and on emissions of Cd and NOx is analyzed
Wildegger-Gaissmaier, Anna Elisabeth. "Fluidized bed utilization of South Australian coals / Anna Elisabeth Wildegger-Gaissmaier". Thesis, 1988. http://hdl.handle.net/2440/18806.
Pełny tekst źródłaChin, Ming Chu, i 秦銘助. "The Mathematical Model of Coal Combustion in the Vortexing Fluidized Bed Combustor". Thesis, 1994. http://ndltd.ncl.edu.tw/handle/32302461555629449088.
Pełny tekst źródła中原大學
化學工程研究所
82
A novel dimensionless relationship for predicting the proportions of volatile combustion within different regions of the fluidized bed combustor was presented. The temperatures of different regions can be predicted by material and energy balance including the proportion of volatile combustion. Experiments were carried out in a 0.45m pilot vortexing fluidized bed combustor (VFBC) to obtain temperature data of the two coal particle sizes, 2.52mm and 6.68mm, with different operating conditions. By using the multiple linear regression, the constants of the dimension- less equation were calculated. This model was used to predict the temperature distribution of the 0.7m*1.4m prototype VFBC and the difference between the experimental and theoretical study was compared. When the primary air increases, the temperature distribution curve stays the same and the total temperature decreases; the temperature of the freeboard decreases as the secondary air increases and the temperature has little increase both in the bed and above bed surface. The 6.68mm coal particle's temperature in the freeboard is lower than in the bed and compared with the 2.52mm coal particle, it shows a higher proportion of volatile combustion in the bed. The 2.52mm coal particle's temperature is higher at the feed position than in the bed because the time of volatile release is short due to the small particle size. Although the theoretical temperature is sometimes higher or sometimes lower than the experimental value, but the tendency of both are the same. The difference is smaller than 20℃ and the average deviation of including operating condition of the pilot and prototype VFBC doesn't exceed 7% within the three regions. The predictions from the model of different primary/ theoretical air ratio and different particle size also coincide well.
Książki na temat "Fluidized-bed combustion Mathematical models"
Hyppänen, Timo. An experimental and theoretical study of multiphase flow in a circulating fluidized bed. Lappeenranta: Lappeenranta University of Technology, 1989.
Znajdź pełny tekst źródłaKo, Daekwun. A numerical study of solid fuel combustion in a moving bed. 1993.
Znajdź pełny tekst źródłaRhee, Brian Kanghee. Enhancement of mass transfer coefficient in three-phase magnetically stabilized fluidized bed. 1998.
Znajdź pełny tekst źródłaJovanovic, Zoran R. Kinetic study on the production of silicon nitride by direct nitridation of silicon in a fluidized bed: Experiment and modeling. 1994.
Znajdź pełny tekst źródłaCzęści książek na temat "Fluidized-bed combustion Mathematical models"
Steward, F. R. "Mathematical Model of a Circulating Fluidized Bed with Chemical Reaction". W Combustion Technologies for a Clean Environment, 509–28. London: CRC Press, 2022. http://dx.doi.org/10.1201/9780367810597-40.
Pełny tekst źródłade Vicente, S., G. Galiano, J. Velasco i J. M. Aróstegui. "Mathematical Description of the Hydrodynamic Regimes of an Asymptotic Model for Two-Phase Flow Arising in PFBC Boilers". W Proceedings of the 20th International Conference on Fluidized Bed Combustion, 870–76. Berlin, Heidelberg: Springer Berlin Heidelberg, 2009. http://dx.doi.org/10.1007/978-3-642-02682-9_135.
Pełny tekst źródłaYang, Chunzhen, Yufeng Duan i Haitao Hu. "DEM-Based Models for Solids Exchange in a Pant Leg Fluidized Bed". W Cleaner Combustion and Sustainable World, 641–49. Berlin, Heidelberg: Springer Berlin Heidelberg, 2012. http://dx.doi.org/10.1007/978-3-642-30445-3_89.
Pełny tekst źródłaButt, A. R., M. G. Jepson i J. Moodie. "Communicating Chemical Processes — A Transputer Model of the British Coal Twin-Bed Pyrolyser/Combustor". W European Consortium for Mathematics in Industry, 95–98. Wiesbaden: Vieweg+Teubner Verlag, 1992. http://dx.doi.org/10.1007/978-3-663-09834-8_14.
Pełny tekst źródłaWeiß, V., J. Schöler i F. N. Fett. "MATHEMATICAL MODELING OF COAL COMBUSTION IN A CIRCULATING FLUIDIZED BED REACTOR". W Circulating Fluidized Bed Technology, 289–98. Elsevier, 1988. http://dx.doi.org/10.1016/b978-0-08-036225-0.50032-0.
Pełny tekst źródłaMiccio, Francesco. "A mathematical model of a fluidized bed combustor coupled with a Stirling engine". W Computer Aided Chemical Engineering, 775–80. Elsevier, 2010. http://dx.doi.org/10.1016/s1570-7946(10)28130-0.
Pełny tekst źródłaDoraiswamy, L. K. "Reactor Design for Solid-Catalyzed Fluid-Phase Reactions". W Organic Synthesis Engineering. Oxford University Press, 2001. http://dx.doi.org/10.1093/oso/9780195096897.003.0019.
Pełny tekst źródłaStreszczenia konferencji na temat "Fluidized-bed combustion Mathematical models"
Mei, Joseph S., Esmail R. Monazam i Lawerence J. Shadle. "The Mapping of Flow Regimes for a Light Material: Cork". W 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-014.
Pełny tekst źródłaMueller, Christian, Anders Brink i Mikko Hupa. "Numerical Simulation of the Combustion Behavior of Different Biomasses in a Bubbling Fluidized Bed Boiler". W 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78138.
Pełny tekst źródłaMonazam, Esmail R., i Lawrence J. Shadle. "Fuel Gas Clean-Up in a Transport Reactor: Model Development and Analysis". W 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78082.
Pełny tekst źródłaAda´nez, Juan, Francisco Garci´a-Labiano, Luis F. de Diego, Ainhoa Plata, Javier Celaya, Pilar Gaya´n i Alberto Abad. "Optimizing the Fuel Reactor for Chemical Looping Combustion". W 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-063.
Pełny tekst źródłaAda´nez, Juan, Luis F. de Diego, Pilar Gaya´n, Francisco Garci´a-Labiano, Andre´s Cabanillas i Alberto Bahillo. "Co-Combustion of Biomass and Coal in Circulating Fluidized Bed: Modeling and Validation". W 17th International Conference on Fluidized Bed Combustion. ASMEDC, 2003. http://dx.doi.org/10.1115/fbc2003-064.
Pełny tekst źródłaZ˙ukowski, Witold. "Methane and Ethane Combustion in an Inert Fluidized Bed". W 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78100.
Pełny tekst źródłaYusof, Nurul Syazwani, Sumarni Abu Bakar i Razidah Ismail. "Modified graphical autocatalytic set model of combustion process in circulating fluidized bed boiler". W PROCEEDINGS OF THE 21ST NATIONAL SYMPOSIUM ON MATHEMATICAL SCIENCES (SKSM21): Germination of Mathematical Sciences Education and Research towards Global Sustainability. AIP Publishing LLC, 2014. http://dx.doi.org/10.1063/1.4887567.
Pełny tekst źródłaNakamura, Masato, Hanwei Zhang, Karsten Millrath i Nickolas J. Themelis. "Modeling of Waste-to-Energy Combustion With Continuous Variation of the Solid Waste Fuel". W ASME 2003 International Mechanical Engineering Congress and Exposition. ASMEDC, 2003. http://dx.doi.org/10.1115/imece2003-55342.
Pełny tekst źródłaMastrovito, M., S. M. Camporeale, A. Forte i B. Fortunato. "Analysis of Pressure Oscillations Data in Gas Turbine Annular Combustion Chamber Equipped With Passive Damper". W ASME Turbo Expo 2005: Power for Land, Sea, and Air. ASMEDC, 2005. http://dx.doi.org/10.1115/gt2005-69056.
Pełny tekst źródłaYue, Guangxi, Junfu Lu, Hai Zhang, Hairui Yang, Jiansheng Zhang, Qing Liu, Zheng Li, Eric Joos i Philippe Jaud. "Design Theory of Circulating Fluidized Bed Boilers". W 18th International Conference on Fluidized Bed Combustion. ASMEDC, 2005. http://dx.doi.org/10.1115/fbc2005-78134.
Pełny tekst źródłaRaporty organizacyjne na temat "Fluidized-bed combustion Mathematical models"
Preto, F. A mathematical model for fluidized bed coal combustion. Natural Resources Canada/ESS/Scientific and Technical Publishing Services, 1985. http://dx.doi.org/10.4095/302616.
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